Recombinant α-L-iduronidase, methods for producing and purifying the same and methods for treating diseases caused by deficiencies thereof

ABSTRACT

The present invention provides a recombinant human alpha-L-iduronidase and biologically active fragments and mutants thereof, large scale methods to produce and purify commercial grade recombinant human alpha-L-iduronidase enzyme as well as methods to treat certain genetic disorders including alpha-L-iduronidase deficiency and mucopolysaccharidosis I (MPS 1).

This application is a continuation-in-part of U.S. patent applicationSer. No. 09/439,923, filed on Nov. 12, 1999 now U.S. Pat. No. 6,426,208,Jul. 30, 20002.

FIELD OF THE INVENTION

The present invention is in the field of molecular biology, enzymology,biochemistry and clinical medicine. In particular, the present inventionprovides a human recombinant α-L-iduronidase, methods of large-scaleproduction and purification of commercial grade human recombinantα-L-iduronidase enzyme, and methods to treat certain genetic disordersincluding α-L-iduronidase deficiency and mucopolysaccharidosis I (MPSI).

BACKGROUND OF THE INVENTION

Carbohydrates play a number of important roles in the functioning ofliving organisms. In addition to their metabolic roles, carbohydratesare structural components of the human body covalently attached tonumerous other entities such as proteins and lipids (calledglycoconjugates). For example, human connective tissues and cellmembranes comprise proteins, carbohydrates and a proteoglycan matrix.The carbohydrate portion of this proteoglycan matrix provides importantproperties to the body's structure.

A genetic deficiency of the carbohydrate-cleaving, lysosomal enzymeα-L-iduronidase causes a lysosomal storage disorder known asmucopolysaccharidosis I (MPS I) (Neufeld and Muenzer, pp. 1565-1587, inThe Metabolic Basis of Inherited Disease, Eds., C. R. Scriver, A. L.Beaudet, W. S. Sly, and D. Valle, McGraw-Hill, New York (1989)) In asevere form, MPS I is commonly known as Hurler syndrome and isassociated with multiple problems such as mental retardation, cloudingof the cornea, coarsened facial features, cardiac disease, respiratorydisease, liver and spleen enlargement, hernias, and joint stiffness.Patients suffering from Hurler syndrome usually die before age 10. In anintermediate form known as Hurler-Scheie syndrome, mental function isgenerally not severely affected, but physical problems may lead to deathby the teens or twenties. Scheie syndrome is the mildest form of MPS I.It is compatible with a normal life span, but joint stiffness, cornealclouding and heart valve disease cause significant problems.

The frequency of MPS I is estimated to be 1:100,000 according to aBritish Columbia survey of all newborns (Lowry, et al., Human Genetics85:389-390 (1990)) and 1:70,000 according to an Irish study (Nelson,Human Genetics 101:355-358 (1990)). There appears to be no ethnicpredilection for this disease. It is likely that worldwide the diseaseis underdiagnosed either because the patient dies of a complicationbefore the diagnosis is made or because the milder forms of the syndromemay be mistaken for arthritis or missed entirely. Effective newbornscreening for MPS I would likely find some previously undetectedpatients.

Except for a few patients which qualify for bone marrow transplantation,there are no significant therapies available for all MPS I patients.Hobbs, et al. (Lancet 2: 709-712 (1981)) first reported that bone marrowtransplantation successfully treated a Hurler patient. Since that time,clinical studies at several transplant centers have shown improvement inphysical disease and slowing or stabilizing of developmental decline ifperformed early. (Whitley, et al., Am. J. Med. Genet. 46: 209-218(1993); Vellodi, et al., Arch. Dis. Child. 76: 92-99 (1997); Peters, etal., Blood 91: 2601-2608 (1998); Guffon, et al., J. Pediatrics 133:119-125 (1998)) However, the significant morbidity and mortality, andthe need for matched donor marrow, limits the utility of bone marrowtransplants. An alternative therapy available to all affected patientswould provide an important breakthrough in treating and managing thisdisease.

Enzyme replacement therapy has been considered a potential therapy forMPS I following the discovery that α-L-iduronidase can correct theenzymatic defect in Hurler cells in culture, but the development ofhuman therapy has been technically unfeasible until now. In thecorrective process, the enzyme containing a mannose-6-phosphate residueis taken up into cells through receptor-mediated endocytosis andtransported to the lysosomes where it clears the stored substrates,heparan sulfate and dermatan sulfate. Application of this therapy tohumans has previously not been possible due to inadequate sources ofα-L-iduronidase in tissues.

For α-L-iduronidase enzyme therapy in MPS I, a recombinant source ofenzyme has been needed in order to obtain therapeutically sufficientsupplies of the enzyme. The cDNA for the canine enzyme was cloned in1991 (Stoltzfus, et al., J. Biol. Chem. 267:6570-6575 (1992) and for thehuman enzyme in the same year. (Scott, et al., Proc. Natl. Acad. Sci.U.S.A. 88:9695-9699 (1991), Moskowitz, et al., FASEB J 6:A77 (1992)).Following the cloning of cDNA for α-L-iduronidase, the production ofadequate quantities of recombinant α-L-iduronidase allowed the study ofenzyme replacement therapy in canine MPS I. (Kakkis, et al., ProteinExpr. Purif. 5: 225-232 (1994)) Enzyme replacement studies in the canineMPS I model demonstrated that intravenously-administered recombinantα-L-iduronidase distributed widely and reduced lysosomal storage frommany tissues. (Shull, et al., Proc. Natl. Acad. Sci. U.S.A. 91:12937-12941 (1994); Kakkis, et al., Biochem. Mol. Med. 58: 156-167(1996)).

BRIEF SUMMARY OF THE INVENTION

In one aspect, the present invention features a method to mass producehuman recombinant α-L-iduronidase in large scale amounts withappropriate purity to enable large scale production for long termpatient use of the enzyme therapy. In a broad embodiment, the methodcomprises the step of transfecting a cDNA encoding for all or part of anα-L-iduronidase into a cell suitable for the expression thereof. In someembodiments, a cDNA encoding for a complete α-L-iduronidase is used,preferably a human α-L-iduronidase. However, in other embodiments, acDNA encoding for a biologically active fragment or mutant thereof maybe used. Specifically, one or more amino acid substitutions may be madewhile preserving or enhancing the biological activity of the enzyme. Inother preferred embodiments, an expression vector is used to transferthe cDNA into a suitable cell or cell line for expression thereof. Inone particularly preferred embodiment, the cDNA is transfected into aChinese hamster ovary cell to create cell line 2.131. In yet otherpreferred embodiments, the production procedure features one or more ofthe following characteristics which have demonstrated particularly highproduction levels: (a) the pH of the cell growth culture may be loweredto about 6.5 to 7.0, preferably to about 6.8-7.0 during the productionprocess, (b) as many as 2 to 3.5 culture volumes of the medium may bechanged during each 24-hour period by continuous perfusion, (c) oxygensaturation may be optimized to about 40% but may be as high as 80%, (d)macroporous cellulose microcarriers with about 5% serum in the mediuminitially, may be used to produce cell mass followed by a rapid washoutshift to protein-free medium for production, (e) a protein-free or lowprotein-medium such as a JRH Biosciences PF-CHO product may be optimizedto include supplemental amounts of one or more ingredients selected fromthe group consisting of: glutamate, aspartate, glycine, ribonucleosides,and deoxyribonucleosides; (f) a stirred tank suspension culture may beperfused in a continuous process to produce iduronidase.

In a second aspect, the present invention provides a transfected cellline which features the ability to produce α-L-iduronidase in amountswhich enable using the enzyme therapeutically. In preferred embodiments,the present invention features a recombinant Chinese hamster ovary cellline such as the 2.131 cell line that stably and reliably producesamounts of α-L-iduronidase which enable using the enzymetherapeutically. In some preferred embodiments, the cell line maycontain more than 1 copy of an expression construct. In even morepreferred embodiments, the cell line expresses recombinantα-L-iduronidase in amounts of at least 20 micrograms per 10⁷ cells perday.

In a third aspect, the present invention provides novel vectors suitableto produce α-L-iduronidase in amounts which enable using the enzymetherapeutically. In preferred embodiments, the present inventionfeatures an expression vector comprising a cytomegaloviruspromoter/enhancer element, a 5′ intron consisting of a murine Cα intron,a cDNA encoding all or a fragment or mutant of an a α-L-iduronidase, anda 3′ bovine growth hormone polyadenylation site. Also, preferably thecDNA encoding all or a fragment or mutant of an α-L-iduronidase is about2.2 kb in length. This expression vector may be transfected at, forexample, a 50 to 1 ratio with any appropriate common selection vectorsuch as pSV2NEO, to enhance multiple copy insertions. Alternatively,gene amplification may be used to induce multiple copy insertions.

In a fourth aspect, the present invention provides novel α-L-iduronidaseproduced in accordance with the methods of the present invention andthereby present in amounts which enable using the enzymetherapeutically. The specific activity of the α-L-iduronidase accordingto the present invention is in excess of 200,000 units per milligramprotein. Preferably, it is in excess of about 240,000 units permilligram protein. The molecular weight of the α-L-iduronidase of thepresent invention is about 82,000 daltons, about 70,000 daltons beingamino acid, and about 12,000 daltons being carbohydrates.

In a fifth aspect, the present invention features a novel method topurify α-L-iduronidase. According to a first embodiment, a cell mass maybe grown in about 5% serum-containing medium, followed by a switch to amodified protein-free production medium without any significantadaptation to produce a high specific activity starting material forpurification. In one preferred embodiment, a three step columnchromatography may be used to purify the enzyme. Such a three stepcolumn chromatography may include using a blue sepharose FF, a Cu++chelating sepharose chromatography and a phenyl sepharose HPchromatography. In another preferred embodiment, an acid pH treatmentstep is used to inactivate potential viruses without harming the enzyme.Concanavalin A-Sepharose, Heparin-Sepharose and Sephacryl 200 columnsare removed and Blue-Sepharose and copper chelating columns added toincrease the capacity of the large scale purification process, to reduceundesirable leachables inappropriate for long term patient use, and toimprove the purity of the product.

In a sixth aspect, the present invention features novel methods oftreating diseases caused all or in part by a deficiency inα-L-iduronidase. In one embodiment, this method features administering arecombinant α-L-iduronidase or a biologically active fragment or mutantthereof alone or in combination with a pharmaceutically suitablecarrier. In other embodiments, this method features transferring anucleic acid encoding all or a part of an α-L-iduronidase into one ormore host cells in vivo. Preferred embodiments include optimizing thedosage to the needs of the organism to be treated, preferably mammals orhumans, to effectively ameliorate the disease symptoms. In preferredembodiments, the disease is Mucopolysaccharidosis I (MPS I), Hurlersyndrome, Hurler-Scheie syndrome or Scheie syndrome.

In a seventh aspect, the present invention features novel pharmaceuticalcompositions comprising α-L-iduronidase useful for treating a diseasecaused all or in part by a deficiency in α-L-iduronidase. Suchcompositions may be suitable for administration in a number of ways suchas parenteral, topical, intranasal, inhalation or oral administration.Within the scope of this aspect are embodiments featuring nucleic acidsequences encoding all or a part of an α-L-iduronidase which may beadministered in vivo into cells affected with an α-L-iduronidasedeficiency.

DESCRIPTION OF THE FIGURES

FIG. 1 represents the nucleotide and deduced amino acid sequences ofcDNA encoding α-L-iduronidase (SEQ ID NOS:1 and 2). Nucleotides 1through 6200 are provided. Amino acids are provided starting with thefirst methionine in the open reading frame.

FIG. 2 represents the results from SDS-PAGE runs of eluate obtainedaccording to the procedures as described below. The top panel shows theSDS-PAGE results of purified α-L-iduronidase (3 micrograms) andcontaminants from the production/purification scheme disclosed inKakkis, et al., Protein Expr. Purif. 5: 225-232 (1994). In the bottompanel, SDS-PAGE results of purified α-L-iduronidase with contaminantsfrom an unpublished prior production/purification process (U.S. patentapplication Ser. Nos. 09/078,209 and 09/170,977) referred to as theCarson method in Lanes 2 (7.5 microgram α-L-iduronidase) and Lane 3 (5.0microgram α-L-iduronidase) are compared to that of theproduction/purification process of the present invention referred to asthe Galli Process (Lane 4 5 micrograms α-L-iduronidase). Lane 1 containsthe molecular weight marker. FIG. 2 shows that the Galliproduction/purification method of the present invention yields a highlypurified α-L-iduronidase product with fewer contaminants in comparisonwith prior production/purification schemes.

FIGS. 3A, 3B demonstrates the α-iduronidase production level over a30-day period, during which time cells are switched at day 5 from aserum—containing medium to a serum-free medium. α-Iduronidase productionwas characterized by: (1) absence of a need for adaptation when cellsare switched from serum-containing to serum-free medium at 100200 (topand bottom panels) with an uninterrupted increase in productivity (toppanel); (2) a high level of production in excess of 4 mg per liter (1000per mL) in a protein-free medium (bottom panel); and (3) a boost inα-iduronidase production with butyrate induction events (bottom panel).

FIG. 4 demonstrates a decrease in liver volume during enzyme therapy inMPS I patients.

FIG. 5 demonstrates urinary GAG excretion during enzyme therapy.

FIG. 6 demonstrates elbow and knee extension in HAC002 during enzymetherapy.

FIG. 7 demonstrates shoulder flexion to 104 weeks in four patients withthe most restriction during enzyme therapy.

FIG. 8 demonstrates improvement in sleep apnea before and after sixweeks of therapy.

FIG. 9 demonstrates the improvement in apneas and hypopneas during sleepwith enzyme therapy in each individual patient.

FIG. 10 demonstrates the improvement in pulmonary function tests beforeand after 12 and 52 weeks of enzyme therapy in one patient.

FIG. 11 demonstrates increased height growth velocity with enzymetherapy.

FIG. 12 shows the degree of contamination by Chinese Hamster OvaryProtein (CHOP) and degree of purity of α-L-iduronidase, produced by (1)the Carson method, an unpublished prior production/purification process(U.S. patent application Ser. Nos. 09/078,209 and 09/170,977 and (2) theGalli method, the production/purification process of the presentinvention. Thus, FIG. 12 shows that α-L-iduronidase produced andpurified by the Galli method has a higher degree of purity and lowerdegree of CHOP contamination in comparison to that of the Carson method.

DETAILED DESCRIPTION OF THE INVENTION

In one aspect, the present invention features a method to produceα-L-iduronidase in amounts which enable using the enzymetherapeutically. In general, the method features transforming a suitablecell line with the cDNA encoding for all of α-L-iduronidase or abiologically active fragment or mutant thereof. Those of skill in theart may prepare expression constructs other than those expresslydescribed herein for optimal production of α-L-iduronidase in suitablecell lines transfected therewith. Moreover, skilled artisans may easilydesign fragments of cDNA encoding biologically active fragments andmutants of the naturally occurring α-L-iduronidase which possess thesame or similar biological activity to the naturally occurringfull-length enzyme.

To create a recombinant source for α-L-iduronidase, a large series ofexpression vectors may be constructed and tested for expression of aα-L-iduronidase cDNA. Based on transient transfection experiments, aswell as stable transfections, an expression construct may be identifiedthat provides a particularly high level of expression. In one embodimentof the present invention, a Chinese hamster cell line 2.131 developed bytransfection of the α-L-iduronidase expression construct and selectionfor a high expression clone provides particularly high level expression.Such a Chinese hamster cell line according to this embodiment of thepresent invention may secrete about 5,000 to 7,000 fold moreα-L-iduronidase than normal. The α-L-iduronidase produced thereby may beproperly processed, taken up into cells with high affinity and iscorrective for α-L-iduronidase deficient cells, such as those frompatients suffering from Hurler's Syndrome.

The method for producing α-L-iduronidase in amounts that enable usingthe enzyme therapeutically features a production process specificallydesigned to mass produce commercial grade enzyme, wherein the quality ofthe enzyme has been deemed acceptable for administration to humans byregulatory authorities of various countries. The large scale productionof commercial grade enzyme necessitates modifications of the cellculture scale, microcarrier systems, and purification scheme. Inpreferred embodiments, the cell culture scale is increased from 45liters to 110 liters or more, with a change to continuous perfusion. Theincrease in scale is necessary to produce sufficient material forpotential large scale production for long term patient use. According topreferred embodiments of such a process, microcarriers are used as a lowcost scalable surface on which to grow adherent cells. In particularlypreferred embodiments, such microcarriers are macroporous and arespecifically composed of modified carbohydrates such as cellulose, e.g.,Cytopore beads manufactured by Pharmacia. Macroporous cellulosemicrocarriers allow improved cell attachment and provide a largersurface area for attachment, which is expected to yield an increasedcell density during the culture process. Higher cell densities areexpected to increase productivity. In preferred embodiments,heparin-Sepharose and Sephacryl 200 columns are replaced withBlue-Sepharose and Copper chelating columns to increase the capacity ofthe large scale purification process and to improve the purity of theproduct. In a particularly preferred embodiment, the copper chelatingcolumn is used to reduce Chinese hamster ovary cell protein contaminantsto very low levels appropriate for large scale distribution. Usingembodiments of the present method featuring modifications and inductiondescribed below, approximately 15 mg per liter of culture per day, ormore at peak culturing density can be produced starting with a 110 literculture system.

According to other preferred embodiments of the method for producingα-L-iduronidase according to the present invention, a culture system isoptimized. In a first embodiment, the culture pH is lowered to about 6.5to 7.0, preferably to about 6.7-7.0 during the production process. Oneadvantage of such a pH is to enhance accumulation of lysosomal enzymesthat are more stable at acidic pH. In a second embodiment, as many as 2to 3.5 culture volumes of the medium may be changed during each 24-hourperiod by continuous perfusion. One advantage of this procedure is toenhance the secretion rate of recombinant α-L-iduronidase and to capturemore active enzyme. In a third embodiment, oxygen saturation isoptimized at about 40%. In a fourth embodiment, macroporousmicrocarriers with about 5% serum initially in the medium, are used toproduce a cell mass followed by a rapid washout shift to a protein-freemedium for production (FIG. 3). In a fifth embodiment, a protein-freegrowth medium, such as a JRH Biosciences PF-CHO product, may beoptimized to include supplemental amounts of one or more ingredientsselected from the group consisting of: glutamate, aspartate, glycine,ribonucleosides and deoxyribonucleosides. In a sixth embodiment, as manyas 2 to 3.5 culture volumes of the medium may be changed during each24-hour period by continuous perfusion. Such an induction process mayprovide about a two-fold increase in production without significantlyaltering post-translational processing.

Particularly preferred embodiments of the method for producingα-L-iduronidase according to the present invention feature one, morethan one, or all of the optimizations described herein and may beemployed as described in more detail below. The production method of thepresent invention may, therefore, provide a production culture processhaving the following features:

1. A microcarrier based culture using macroporous microcarrier beadsmade of modified cellulose or an equivalent thereof is preferably usedin large scale culture flasks with overhead stirring or an equivalentthereof. Attachment of cells to these beads may be achieved by culturein a 5% fetal bovine serum may be added to DME/F12 1:1 or a protein-freemedium modified with ingredients including ribonucleosides,deoxyribonucleosides, pyruvate, non-essential amino acids, and HEPES.After about 3-6 days in this medium, a washout procedure is begun inwhich protein-free medium replaces the serum-containing medium at anincreasing perfusion rate dependent on the glucose content and culturecondition. Subsequently, and throughout the entire remaining cultureperiod, the cells are cultivated in a protein-free medium. The use of aprotein-free medium in enzyme production is beneficial in reducing theexposure risk of bovine spongiform encephalopathy (BSE) and otherinfectious biologic agents such as viruses to patients being treatedwith the enzyme, wherein the risk of BSE or other harmful agents isdependent on the amount of potential serum exposure. In prior publishedstudies, the carriers used to grow the cells were bovine gelatinmicrocarriers, used at 1 gram per liter or 100 times the productconcentration. Leaching of 1% of the gelatin protein from themicrocarriers would represent a relative 100% contamination and therebycontribute to the risk of BSE. Thus, new carriers are either dextran orcellulose-based and consist of carbohydrates, and not animal-derivedmaterials.

FIG. 3 shows that the cells are grown to a density in 5% serumcontaining medium and then switched without any adaptation to aprotein-free medium. FIG. 3 specifically shows that: 1) Cells surviveand continue to produce iduronidase when shifted without adaptation. Incontrast, other studies would suggest that adaptation to a protein-freemedium is necessary. In the method of the present invention, enzymeproduction continues at levels comparable to serum containing medium. 2)α-L-Iduronidase produced in a protein-free medium retains a level ofproduction in excess of 4 mg per liter or 1,000 units per ml. 3)α-L-Iduronidase produced in a protein-free medium has high uptakeindicating that the shift in medium and, hence, a shift in carbohydratesbeing fed to cells, does not adversely affect the high uptake characterof the enzyme. Eight lots of α-L-iduronidase have been produced andreleased in this manner with an uptake half maximal value of less than 2nM in all lots.

2. The culture conditions are preferably maintained at a dissolvedoxygen of 40% of air saturation at a pH of about 6.8-7.0 and at atemperature of about 35-37° C. This may be achieved using a controlunit, monitoring unit and appropriate probes such as those produced byApplikon® or Mettler®. However, skilled artisans will readily appreciatethat this can easily be achieved by equivalent control systems producedby other manufacturers. An air saturation of about 40% results inimproved α-L-iduronidase secretion though up to 80%% air saturation maybe used. However, further increases in oxygen to, for example, 90% airsaturation, do not provide significantly enhanced secretion over 80% airsaturation. The dissolved oxygen may be supplied by intermittent orcontinuous oxygen sparging using a 5 micron stainless steel or largeropening sparger, or equivalent thereof. A pH of about 6.8-7.0 is optimalfor the accumulation of the α-L-iduronidase enzyme. The enzyme isparticularly unstable at pHs above about 7.0. Below a pH of about 6.7,the secretion rate may decrease, particularly below a pH of about 6.5.The culture is therefore maintained optimally between a pH of about6.8-7.0.

3. The production culture medium may be a modified form of thecommercially available proprietary medium from JRH Biosciences calledExcell PF CHO. This medium supports levels of secretion equivalent tothat of serum using a cell line such as the 2.131 cell line. It may bepreferably modified to include an acidic pH of about 6.8-7.0 (±0.1), andbuffered with HEPES at 7.5 mM or 15 mM. The medium may contain 0.05 to0.1% of Pluronics F-68 (BASF), a non-ionic surfactant or an equivalentthereof which features the advantage of protecting cells from shearforces associated with sparging. The medium may further contain aproprietary supplement that is important in increasing the productivityof the medium over other protein-free media that are presentlyavailable. Those skilled in the art will readily understand that thechoice of culture medium may be optimized continually according toparticular commercial embodiments available at particular points intime. Such changes encompass no more than routine experimentation andare intended to be within the scope of the present invention.

4. The production medium may be analyzed using an amino acid analyzercomparing spent medium with starting medium. Such analyses havedemonstrated that the 2.131 cell line depletes a standard PF CHO mediumof glycine, glutamate and aspartate to a level of around 10% of thestarting concentration. Supplementation of these amino acids to higherlevels may result in enhanced culture density and productivity that maylead to a 2-3 fold higher production than at baseline. Skilled artisanswill appreciate that other cell lines within the scope of the presentinvention may be equally useful for producing α-L-iduronidase accordingto the present method. Hence, more or less supplemental nutrients may berequired to optimize the medium. Such optimizations are intended to bewithin the scope of the present invention and may be practiced withoutundue experimentation.

5. The medium may be supplemented with the four ribonucleosides and fourdeoxyribonucleosides each at about 10 mg/liter to support thedihydrofolate reductase deficient cell line 2.131. Skilled artisans willappreciate that other cell lines within the scope of the presentinvention may be equally useful for producing α-L-iduronidase accordingto the present method. Hence, more or less ribonucleosides anddeoxyribonucleosides may be required to optimize the medium, andalternative sources of purines and pyrmidines for nucleic acid synthesismay be used such as hypoxanthine and thymidine. Such optimizations areintended within the scope of the present invention and may be practicedwithout undue experimentation.

6. After reaching confluence at about 3-6 days of culture, an increasingrate of continuous perfusion is initiated. A change of medium may beaccomplished, for example, using a slant feed tube constructed andpositioned to allow the uptake of medium without removal of themicrocarriers even while the culture is stirred. By pumping out mediumthrough the slant feed tube, microcarriers settle within the body of thetube inside the culture and are not removed from the culture during thechange on medium. In this manner, the microcarriers with the cell massare separated from supernatant containing the enzyme.

7. The rapid and frequent turnover of the medium has been shown byproductivity studies to result in improved overall collection of enzymefrom the cell culture. Less turnover of medium results in less totalproduction of enzyme on a daily basis. Using the perfusion of 2-3.5culture volumes per day, the cells may be maintained in excellentcondition with high degrees of viability and a high level ofproductivity.

8. Production of α-L-iduronidase may be enhanced by the use of sodiumbutyrate induction of gene expression (FIG. 3). Twenty lots ofα-L-iduronidase were produced using butyrate induction at 2 nMconcentration with 2/3 washout every 12 hours after induction andreinduction every 48 hours for a 21-day production period. In FIG. 3,the vertical arrows at the bottom indicate butyrate induction events.Each induction triggered a boost in α-L-iduronidase concentration in themedium.

Systematic studies of a 2.131 cell line demonstrated that about 2 mMbutyrate can be applied and result in about a two-fold or greaterinduction of enzyme production with minimal effects on carbohydrateprocessing. Lower levels of butyrate have not been shown to induce aswell, and substantially higher levels may result in higher induction,but declining affinity of the produced enzyme for cells from patientssuffering from α-L-iduronidase deficiency. Butyrate induction performedin vitro at 2 mM for 24 hours or 5 mM, a more commonly usedconcentration resulted in uptakes in excess of 3 nM or 40 U/ml, or anaverage of three times the value observed in production lots. Inaddition, commonly used times of 24 hours or more and concentration of 5mM were toxic to α-L-iduronidase producing cells and resulted indetachment and loss of cell mass.

Results suggest that two-fold or greater induction results in lessprocessing of the carbohydrates and less phosphate addition to theenzyme, as well as increasing toxicity. With respect to carbohydrateprocessing and the addition of phosphate groups, the importance ofmannose-6-phosphate in enzyme replacement therapy is demonstrated by theobservations that removal of the phosphate of two lysosomal enzymes,glucosidase and galactosamine 4-sulfatase leads to decreased uptake (Vander Ploeg, et al., J. Clin. Invest. 87: 513-518 (1991); Crawley, et al.,J. Clin. Invest. 97: 1864-1873 (1996)). In addition, enzyme with lowphosphate (Van Hove, et al., Proc. Natl. Acad. Sci. USA 93: 65-70 (1996)requires 1,000 units per ml for uptake experiments (nearly 100 timesused for iduronidase) and effective doses in animal models require 14mg/kg, or 28 times the dose used with high phosphate containingiduronidase (Kikuchi, et al., J. Clin. Invest. 101: 827-833.(1998)).

One particularly preferred aspect of the invention method uses 2 mMbutyrate addition every 48 hours to the culture system. This embodimentresults in about a two-fold induction of enzyme production using thismethod without significant effect on the uptake affinity of the enzyme(K-uptake of less than 30 U/ml or 2.0 mM).

9. In a second aspect, the present invention provides a transfected cellline, which possesses the unique ability to produce α-L-iduronidase inamounts, which enable using the enzyme therapeutically. In preferredembodiments, the present invention features a recombinant Chinesehamster ovary cell line such as the 2.131 cell line that stably andreliably produces amounts of α-L-iduronidase. In preferred embodiments,the cell line may contain more than 1 copy of an expression constructcomprising a CMV promoter, a Ccc intron, a human α-L-iduronidase cDNA,and a bovine growth hormone polyadenylation sequence. In even morepreferred embodiments, the cell line expresses α-L-iduronidase atamounts of at least about 20-40 micrograms per 10⁷ cells per day in aproperly processed, high uptake form appropriate for enzyme replacementtherapy. According to preferred embodiments of this aspect of theinvention, the transfected cell line adapted to produce α-L-iduronidasein amounts which enable using the enzyme therapeutically, possesses oneor more of the following features:

1. The cell line of preferred embodiments is derived from a parent cellline wherein the cells are passaged in culture until they have acquireda smaller size and more rapid growth rate and until they readily attachto substrates.

2. The cell line of preferred embodiments is transfected with anexpression vector containing the cytomegalovirus promoter/enhancerelement, a 5′ intron consisting of the murine Cα intron between exons 2and 3, a human cDNA of about 2.2 kb in length, and a 3′ bovine growthhormone polyadenylation site. This expression vector may be transfectedat, for example, a 50 to 1 ratio with any appropriate common selectionvector such as pSV2NEO. The selection vector pSV2NEO in turn confersG418 resistance on successfully transfected cells. In particularlypreferred embodiments, a ratio of about 50 to 1 is used since this ratioenhances the acquisition of multiple copy number inserts. According toone embodiment wherein the Chinese hamster ovary cell line 2.131 isprovided, there is at least 1 copy of the expression vector forα-L-iduronidase. Such a cell line has demonstrated the ability toproduce large quantities of human α-L-iduronidase (minimum 20 microgramsper 10 million cells per day). Particularly preferred embodiments suchas the 2.131 cell line possess the ability to produce properly processedenzyme that contains N-linked oligosaccharides containing high mannosechains modified with phosphate at the 6 position in sufficient quantityto produce an enzyme with high affinity (K-uptake of less than 3 nM).

3. The enzyme produced from the cell lines of the present invention suchas a Chinese hamster ovary cell line 2.131 is rapidly assimilated intocells, eliminates glycosaminoglycan storage and has a half-life of about5 days in cells from patients suffering from α-L-iduronidase deficiency.

4. The cell line of preferred embodiments such as a 2.131 cell lineadapts to large scale culture and stably produces human α-L-iduronidaseunder these conditions. The cells of preferred embodiments are able togrow and secrete α-L-iduronidase at the acid pH of about 6.6 to 7.0 atwhich enhanced accumulation of α-L-iduronidase can occur.

5. Particularly preferred embodiments of the cell line according to theinvention, such as a 2.131 cell line are able to secrete humanα-L-iduronidase at levels exceeding 2,000 units per ml (8 micrograms perml) harvested twice per day or exceeding 15 mg per liter of culture perday using a specially formulated protein-free medium.

In a third aspect, the present invention provides novel vectors suitableto produce α-L-iduronidase in amounts which enable using the enzymetherapeutically. The production of adequate quantities of recombinantα-L-iduronidase is a critical prerequisite for studies on the structureof the enzyme as well as for enzyme replacement therapy. The cell linesaccording to the present invention permit the production of significantquantities of recombinant α-L-iduronidase that is appropriatelyprocessed for uptake. Overexpression in Chinese hamster ovary (CHO)cells has been described for three other lysosomal enzymes,cc-galactosidase (Ioannou, et al., J. Cell. Biol. 119:1137-1150 (1992)),iduronate 2-sulfatase (Bielicki, et al., Biochem. J. 289: 241-246(1993)), and N-acetylgalactosamine 4-sulfatase (Amson, et al., Biochem.J. 284:789-794 (1992)), using a variety of promoters and, in one case,amplification. The present invention features a dihydrofolatereductase-deficient CHO cell line, but according to preferredembodiments of the invention amplification is unnecessary. Additionally,the present invention provides a high level of expression of the humanα-L-iduronidase using the CMV immediate early gene promoter/enhancer.

The present invention features in preferred embodiments, an expressionvector comprising a cytomegalovirus promoter/enhancer element, a 5′intron consisting of the murine Cα intron derived from the murine longchain immunoglobulin Cα gene between exons 2 and 3, a human cDNA ofabout 2.2 kb in length, and a 3′ bovine growth hormone polyadenylationsite. This expression vector may be transfected at, for example, a 50 to1 ratio with any appropriate common selection vector such as pSV2NEO.The selection vector such as pSV2NEO in turn confers G418 resistance onsuccessfully transfected cells. In particularly preferred embodiments, aratio of about 50 to 1 expression vector to selection vector is usedsince this ratio enhances the acquisition of multiple copy numberinserts. According to one embodiment wherein the Chinese hamster ovarycell line 2.131 is provided, there are approximately 10 copies of theexpression vector for α-L-iduronidase. Such an expression construct hasdemonstrated the ability to produce large quantities of humanα-L-iduronidase (minimum 20 micrograms per 10 million cells per day) ina suitable cell line such as a Chinese hamster ovary cell line 2.131.

In a fourth aspect, the present invention provides novel α-L-iduronidaseproduced in accordance with the methods of the present invention andthereby present in amounts that enable using the enzyme therapeutically.The methods of the present invention produce a substantially pureα-L-iduronidase that is properly processed and in high uptake form,appropriate for enzyme replacement therapy and effective in therapy invivo.

The specific activity of the α-L-iduronidase according to the presentinvention is in excess of about 200,000 units per milligram protein.Preferably, it is in excess of about 240,000 units per milligram proteinusing the original assay methods for activity and protein concentration.A novel validated assay for the same enzyme with units expressed asmicromoles per min demonstrates an activity of 100 units/ml (range of70-130) and a protein concentration by absorbance at 280 nM of 0.7 mg/ml(0.6-0.8) with an average specific activity of 143 units per mg. Themolecular weight of the full length α-L-iduronidase of the presentinvention is about 82,000 daltons comprising about 70,000 daltons ofamino acids and 12,000 daltons of carbohydrates. The recombinant enzymeof the present invention is endocytosed even more efficiently than hasbeen previously reported for a partially purified preparation of urinaryenzyme. The recombinant enzyme according to the present invention iseffective in reducing the accumulation of radioactive S-labeled GAG inα-L-iduronidase-deficient fibroblasts, indicating that it is transportedto lysosomes, the site of GAG storage. The remarkably low concentrationof α-L-iduronidase needed for such correction (half-maximal correctionat 0.7 pM) may be very important for the success of enzyme replacementtherapy.

The human cDNA of α-L-iduronidase predicts a protein of 653 amino acidsand an expected molecular weight of 70,000 daltons after signal peptidecleavage. Amino acid sequencing reveals alanine 26 at the N-terminusgiving an expected protein of 629 amino acids. Human recombinantα-L-iduronidase has a Histidine at position 8 of the mature protein. Thepredicted protein sequence comprises six potential N-linkedoligosaccharide modification sites. All of these may be modified in therecombinant protein. The third and sixth sites have been demonstrated tocontain one or more mannose 6-phosphate residues responsible for highaffinity uptake into cells. The following peptide corresponds to AminoAcids 26-45 of Human Recombinant α-L-iduronidase with an N-terminusalanine and the following sequence:

ala-glu-ala-pro-his-leu-val-his-val-asp-ala-ala-arg-ala-leu-trp-pro-leu-arg-arg(part of SEQ ID NO:2)

The overexpression of the α-L-iduronidase of the present invention doesnot result in generalized secretion of other lysosomal enzymes that aredependent on mannose-6-P targeting. The secreted recombinantα-L-iduronidase is similar to normal secreted enzyme in many respects.Its molecular size, found in various determinations to be 77, 82, 84,and 89 kDa, is comparable to 87 kDa, found for urinary corrective factor(Barton et al., J. Biol. Chem. 246: 7773-7779 (1971)), and to 76 kDa and82 kDa, found for enzyme secreted by cultured human fibroblasts(Myerowitz, et al., J. Biol. Chem. 256: 3044-3048 (1991); Taylor, etal., Biochem. J. 274:263-268 (1991)). The differences within and betweenthe studies are attributed to imprecision of the measurements. Thepattern of intracellular processing of the recombinant enzyme, a slowdecrease in molecular size and the eventual appearance of an additionalband smaller by 9 kDa is the same as for the human fibroblast enzyme.This faster band arises by proteolytic cleavage of 80 N-terminal aminoacids.

In a fifth aspect, the present invention features a novel method topurify α-L-iduronidase. In preferred embodiments, the present inventionfeatures a method to purify recombinant α-L-iduronidase that has beenoptimized to produce a rapid and efficient purification with validatiblechromatography resins and easy load, wash and elute operation. Themethod of purifying α-L-iduronidase of the present invention involves aseries of column chromatography steps, which allow the high yieldpurification of enzyme from protein-free production medium.Specifically, Concanavalin A-Sepharose, Heparin-Sepharose and Sephacryl200 columns were replaced with Blue-Sepharose and Copper chelatingcolumns to increase the capacity of a large-scale purification process,to reduce leachables and to improve the purity of the product.Concanavalin A lectin is often used to bind enzyme in an initialpurification step in the prior published study, and is a protein lectinderived from plants. Concanavalin A is known to leach from columns andcontaminate lysosomal enzyme preparations. Such leaching could causeactivation of T cells in treated patients and hence is deemedinappropriate for human administration (Furbish, et al., Proc. Natl.Acad. Sci. USA 74: 3560-3563 (1977)). Thus, the use of Concanavalin A isavoided in the present purification scheme. In a prior study, the humanliver α-L-iduronidase could not be recovered from phenyl columns withouthigh concentrations of detergent (1% Triton X100) denaturation. Hence, aphenyl column was not used in a published purification scheme of thisenzyme (Clements, et al., Eur. J. Biochem. 152: 21-28 (1985). Theendogenous human liver enzyme is highly modified within the lysosomes byhydrolases which remove sialic acid and phosphate residues and proteaseswhich nick the enzyme. In contrast, the overexpression of recombinantα-L-iduronidase causes 50% of the enzyme to be secreted rather thantransported to the lysosome (Zhao, et al., J. Biol. Chem. 272:22758-22765 (1997). Hence, recombinant iduronidase will have a fullarray of sialic acid and phosphate residues, which lead to a higherdegree of water solubility and lower affinity to the phenyl column. Theincreased hydrophilicity allows the enzyme to be eluted undernon-denaturing conditions using the low salt solutions of around 150-700mM NaCl. This feature of the recombinant enzyme allows it to be purifiedin large scale without the use of detergents.

Recombinant α-L-iduronidase over-expressed in a Chinese Hamster Ovary(CHO) cell line, has been purified to near homogeneity following a3-step column chromatography process. The first column involves anaffinity chromatography step using Blue Sepharose 6 FF. The BlueSepharose 6 FF eluate is then further purified by another affinitychromatography step using Cu⁺⁺ Chelating Sepharose FF. The final polishof the highly purified enzyme is achieved by hydrophobic interactionchromatography using Phenyl Sepharose High Performance (HP). Theover-all yield ranges from 45 to 55 percent and the purity of the finalproduct is >99%. The process is robust, reproducible, and scalable forlarge-scale manufacturing. The purified enzyme has been characterizedwith respect to its enzymatic activity using a fluorescence-basedsubstrate, and its functional uptake by fibroblast cells. The enzyme hasalso been characterized for substrate specificity, carbohydrateprofiles, and isoelectric focusing (IEF) profiles.

Particularly preferred embodiments of the method for purifyingα-L-iduronidase according to the present invention feature more than oneor all of the optimizations according to the following particularembodiments. The purification method of the present invention maytherefore provide a purified α-L-iduronidase having the characteristicsdescribed herein.

Outline of the α-L-Iduronidase Purification Process

1. pH Adjustment/Filtration: The pH of filtered harvest fluid (HF) isadjusted to 5.3 with 1 M H₃PO₄ and then filtered through a 0.45μ filter(e.g. Sartoclean, Sartorius).

2. Blue Sepharose FF chromatography: This affinity chromatography stepserves to capture iduronidase to reduce the volume and to purifyiduronidase by approximately seven to ten fold.

Loading capacity: 4 mg/ml (total protein per ml of resin)

Equilibration buffer: 10 mM NaPO₄, pH 5.3

Wash buffer: 400 mM NaCl, 10 mM NaPO₄, pH 5.3

Elution buffer: 0.8 M NaCl, 10 mM NaPO₄, pH 5.3

Regeneration buffer: 2 M NaCl, 10 mM NaPO₄, pH 5.3

Fold of purification: 7-10

Yield: 70-85%

3. Cu⁺⁺ Chelating Sepharose FF chromatography: The Cu⁺⁺ Chelatingaffinity chromatography step is very effective for removing somecontaminating CHO proteins. The inclusion of 10% glycerol in all thebuffers seems to be crucial for the quantitative recovery ofiduronidase.

Loading capacity: 2 mg/ml

Equilibration buffer: 1 M NaCl, 25 mM NaAc, pH 6.0, 10% Glycerol

Wash buffer: 1 M NaCl, 25 mM NaAc, pH 4.0, 10% Glycerol

Elution buffer: 1 M NaCl, 25 mM NaAc, pH 3.7, 10% Glycerol

Regeneration buffer: 1 M NaCl, 50 mM EDTA, pH 8.0

Fold of purification: 2-5

Yield: 80%

4. Phenyl Sephrose HP chromatography: Phenyl Sephrose is used as thelast step to further purify the product as well as to reduce residualleached Cibacron blue dye and Cu⁺⁺ ion carried over from previouscolumns.

Loading capacity: 1 mg/ml

Equilibration buffer: 2 M NaCl, 10 mM NaPO₄, pH 5.7

Wash buffer: 1.5 M NaCl, 10 mM NaPO₄, pH 5.7

Elution buffer: 0.7 M NaCl, 10 mM NaPO₄, pH 5.7

Regeneration buffer: 0 M NaCl, 10 mM NaPO₄, pH 5.7

Fold of purification: 1.5

Yield: 90%

5. Ultrafiltration (UF)/Diafiltration (DF)/Final formulation: Thepurified iduronidase is concentrated and diafiltered to a finalconcentration of 1 mg/ml in formulation buffer (150 mM NaCl, 100 mMNaPO₄, pH 5.8) using a tangential flow filtration (TFF) system (e.g.Sartocon Slice from Sartorius). The enzyme is then sterilized byfiltering through a 0.2-micron filter (e.g., cellulose acetate orpolysulfone) and filled into sterile vials.

6. Characterization of Purified Iduronidase: Analysis of enzyme purityusing SDS-PAGE stained with Coomassie Blue or Silver and Western blotanalysis. Analysis of enzymatic activity using 4MU-sulfate as substrate.Analysis of functional uptake using fibroblast cell assay. Analysis ofcarbohydrates by FACE. Analysis of IEF profiles.

Enzyme purified in this manner has been shown to containmannose-6-phosphate residues of sufficient quantity at positions 3 and 6of the N-linked sugars to give the enzyme uptake affinity of less than30 units per ml (less than 2 nM) enzyme. The enzyme is substantiallycorrective for glycosaminoglycan storage disorders caused by iduronidasedeficiency and has a half-life inside cells of approximately 5 days.

Prior α-L-iduronidase purification schemes (Kakkis, et al., ProteinExpr. Purif. 5: 225-232 (1994); Kakkis, et al., Biochem. Mol. Med. 58:156-167 (1996); U.S. patent application Ser. Nos. 09/078,209 and09/170,977) produced degrees of purity between 90% and less than 99%,which is not optimal for long-term human administration (See FIG. 12).(These and all other U.S. patents herein are specifically incorporatedherein by reference in their entirety.) Treatment with human recombinantα-L-iduronidase with a minimum purity of 97% was associated with someclinical reactions, specifically hives in 5 patients, and complementactivation in 4 patients. All patients demonstrated a reaction to aprotein that is a trace contaminant to the α-L-iduronidase. (FIG. 2)Because this protein exists in both the final product and in theserum-free blank CHO cell line supernatant, the extraneous protein mostlikely originates from the CHO cell. The common proteins that appear tobe activating the clinical allergic response are approximately 60kDaltons and 50 kDaltons respectively, which are too small to berecombinant human iduronidase. Four patients developed an immunereaction to α-L-iduronidase at least transiently as well as to theChinese hamster ovary cell host proteins. It is clear that even thoughthe enzyme used to treat patients is highly purified, the degree ofpurification is important in reducing the immune response tocontaminants. FIG. 2 (SDS-PAGE) and FIG. 12 (CHOP assay) demonstratethat α-L-iduronidase produced and purified by theproduction/purification scheme of the present invention has a higherdegree of purity and lower degree of CHOP contamination in comparison tothat of prior methods of production/purification. Thus, a greater than97% purity is adequate for patient use, higher levels of purity aredesirable and preferable. As shown in FIG. 12, the optimizedpurification scheme described above achieves a degree of purity that isgreater than 99% and importantly reduces Chinese hamster ovary cell hostproteins to less than 1 percent, as determined by the Chinese HamsterOvary Protein (CHOP) assay.

In a sixth aspect, the present invention features novel methods oftreating diseases caused all or in part by a deficiency inα-L-iduronidase. Recombinant α-L-iduronidase provides enzyme replacementtherapy in a canine model of MPS 1. This canine model is deficient inα-L-iduronidase due to a genetic mutation and is similar to human MPS 1.Purified, properly processed α-L-iduronidase was administeredintravenously to 11 dogs. In those dogs treated with weekly doses of25,000 to 125,000 units per kg for 0.5, 3, 6 or 13 months, the enzymewas taken up in a variety of tissues and decreased the lysosomal storagein many tissues. The long term treatment of the disease was associatedwith clinical improvement in demeanor, joint stiffness, coat and growth.Higher doses of therapy (125,000 units per kg per week) result in betterefficacy, including normalization of urinary GAG excretion in additionto more rapid clinical improvement in demeanor, joint stiffness andcoat.

Enzyme therapy at even small doses of 25,000 units (0.1 mg/kg/wk)resulted in significant enzyme distribution to some tissues anddecreases in GAG storage. If continued for over 1 year, some clinicaleffects were evident in terms of increased activity, size and overallappearance of health. The therapy at this dose did not improve othertissues that are important sites for disease in this entity such ascartilage and brain. Higher doses of 125,000 units (0.5 mg/kg) given 5times over two weeks demonstrate that improved tissue penetration can beachieved, and a therapeutic effect at the tissue level was accomplishedin as little as 2 weeks. Studies at this increased dose have beencompleted in two dogs for 15 months. These MPS I dogs are showingsignificant clinical improvement and substantial decreases in urinaryGAG excretion into the near normal range. Other than an immune reactioncontrolled by altered administration techniques, the enzyme therapy hasnot shown significant clinical or biochemical toxicity. Enzyme therapyat this higher weekly dose is effective at improving some clinicalfeatures of MPS I and decreasing storage without significant toxicity.

In a seventh aspect, the present invention features novel pharmaceuticalcompositions comprising human α-L-iduronidase useful for treating adeficiency in α-L-iduronidase. The recombinant enzyme may beadministered in a number of ways such as parenteral, topical,intranasal, inhalation or oral administration. Another aspect of theinvention is to provide for the administration of the enzyme byformulating it with a pharmaceutically acceptable carrier, which may besolid, semi-solid, liquid, or an ingestable capsule. Examples ofpharmaceutical compositions include tablets, drops such as nasal drops,compositions for topical application such as ointments, jellies, creamsand suspensions, aerosols for inhalation, nasal spray, and liposomes.Usually the recombinant enzyme comprises between 0.01 and 99% or between0.01 and 99% by weight of the composition, for example, between 0.01 and20% for compositions intended for injection and between 0.1 and 50% forcompositions intended for oral administration.

To produce pharmaceutical compositions in this form of dosage units fororal application containing a therapeutic enzyme, the enzyme may bemixed with a solid, pulverulent carrier, for example lactose,saccharose, sorbitol, mannitol, a starch such as potato starch, cornstarch, amylopectin, laminaria powder or citrus pulp powder, a cellulosederivative or gelatin and also may include lubricants such as magnesiumor calcium stearate or a Carbowax® or other polyethylene glycol waxesand compressed to form tablets or cores for dragees. If dragees arerequired, the cores may be coated for example with concentrated sugarsolutions which may contain gum arabic, talc and/or titanium dioxide, oralternatively with a film forming agent dissolved in easily volatileorganic solvents or mixtures of organic solvents. Dyestuffs can be addedto these coatings, for example, to distinguish between differentcontents of active substance. For the composition of soft gelatincapsules consisting of gelatin and, for example, glycerol as aplasticizer, or similar closed capsules, the active substance may beadmixed with a Carbowax® or a suitable oil, e.g., sesame oil, olive oil,or arachis oil. Hard gelatin capsules may contain granulates of theactive substance with solid, pulverulent carriers such as lactose,saccharose, sorbitol, mannitol, starches such as potato starch, cornstarch or amylopectin, cellulose derivatives or gelatin, and may alsoinclude magnesium stearate or stearic acid as lubricants.

Therapeutic enzymes of the subject invention may also be administeredparenterally such as by subcutaneous, intramuscular or intravenousinjection or by sustained release subcutaneous implant. In subcutaneous,intramuscular and intravenous injection, the therapeutic enzyme (theactive ingredient) may be dissolved or dispersed in a liquid carriervehicle. For parenteral administration, the active material may besuitably admixed with an acceptable vehicle, preferably of the vegetableoil variety such as peanut oil, cottonseed oil and the like. Otherparenteral vehicles such as organic compositions using solketal,glycerol, formal, and aqueous parenteral formulations may also be used.

For parenteral application by injection, compositions may comprise anaqueous solution of a water soluble pharmaceutically acceptable salt ofthe active acids according to the invention, desirably in aconcentration of 0.01-10%, and optionally also a stabilizing agentand/or buffer substances in aqueous solution. Dosage units of thesolution may advantageously be enclosed in ampules.

When therapeutic enzymes are administered in the form of a subcutaneousimplant, the compound is suspended or dissolved in a slowly dispersedmaterial known to those skilled in the art, or administered in a devicewhich slowly releases the active material through the use of a constantdriving force such as an osmotic pump. In such cases, administrationover an extended period of time is possible.

For topical application, the pharmaceutical compositions are suitably inthe form of an ointment, gel, suspension, cream or the like. The amountof active substance may vary, for example, between 0.05-20% by weight ofthe active substance. Such pharmaceutical compositions for topicalapplication may be prepared in known manner by mixing the activesubstance with known carrier materials such as isopropanol, glycerol,paraffin, stearyl alcohol, polyethylene glycol, etc. Thepharmaceutically acceptable carrier may also include a known chemicalabsorption promoter. Examples of absorption promoters are, e.g.,dimethylacetamide (U.S. Pat. No. 3,472,931), trichloro ethanol ortrifluoroethanol (U.S. Pat. No. 3,891,757), certain alcohols andmixtures thereof (British Patent No. 1,001,949). A carrier material fortopical application to unbroken skin is also described in the Britishpatent specification No. 1,464,975, which discloses a carrier materialconsisting of a solvent comprising 40-70% (v/v) isopropanol and 0-60%(v/v) glycerol, the balance, if any, being an inert constituent of adiluent not exceeding 40% of the total volume of solvent.

The dosage at which the therapeutic enzyme containing pharmaceuticalcompositions are administered may vary within a wide range and willdepend on various factors such as the severity of the disease, the ageof the patient, etc., and may have to be individually adjusted. Apossible range for the amount of therapeutic enzyme which may beadministered per day is about 0.1 mg to about 2000 mg or about 1 mg toabout 2000 mg.

The pharmaceutical compositions containing the therapeutic enzyme maysuitably be formulated so that they provide doses within these ranges,either as single dosage units or as multiple dosage units. In additionto containing a therapeutic enzyme (or therapeutic enzymes), the subjectformulations may contain one or more substrates or cofactors for thereaction catalyzed by the therapeutic enzyme in the compositions.Therapeutic enzymes containing compositions may also contain more thanone therapeutic enzyme.

The recombinant enzyme employed in the subject methods and compositionsmay also be administered by means of transforming patient cells withnucleic acids encoding the recombinant α-L-iduronidase. The nucleic acidsequence so encoded may be incorporated into a vector for transformationinto cells of the subject to be treated. Preferred embodiments of suchvectors are described herein. The vector may be designed so as tointegrate into the chromosomes of the subject, e.g., retroviral vectors,or to replicate autonomously in the host cells. Vectors containingencoding α-L-iduronidase nucleotide sequences may be designed so as toprovide for continuous or regulated expression of the enzyme.Additionally, the genetic vector encoding the enzyme may be designed soas to stably integrate into the cell genome or to only be presenttransiently. The general methodology of conventional genetic therapy maybe applied to polynucleotide sequences encoding α-L-iduronidase.Conventional genetic therapy techniques have been extensively reviewed.(Friedman, Science 244:1275-1281 (1989); Ledley, J. Inherit. Metab. Dis.13:587-616 (1990); Tososhev, et al., Curr Opinions Biotech. 1:55-61(1990)).

A particularly preferred method of administering the recombinant enzymeis intravenously. A particularly preferred composition comprisesrecombinant α-L-iduronidase, normal saline, phosphate buffer to maintainthe pH at about 5.8 and human albumin. These ingredients may be providedin the following amounts:

α-L-iduronidase 0.05-0.2 mg/mL or 12,500-50,000 units per mL

Sodium chloride solution 150 mM in an IV bag, 50-250 cc total volume

Sodium phosphate buffer 10-50 mM, pH 5.8

Human albumin 1 mg/mL

The invention having been described, the following examples are offeredto illustrate the subject invention by way of illustration, not by wayof limitation.

EXAMPLE 1 Producing Recombinant α-L-Iduronidase

Standard techniques such as those described by Sambrook, et al(Molecular Cloning: A Laboratory Manual, 2^(nd) ed., Cold Spring HarborLaboratory, Cold Spring Harbor, N.Y. (1987)) may be used to clone cDNAencoding human α-L-iduronidase. The human α-L-iduronidase cDNApreviously cloned was subcloned into PRCCMV (InVitrogen) as aHindIII-XbaI fragment from a bluescript KS subclone. An intron cassettederived from the murine immunoglobulin Cot intron between exons 2 and 3was constructed using PCR amplification of bases 788-1372 (Tucker, etal., Proc. Natl. Acad. Sci. USA 78: 7684-7688 (1991) of clone pRIR14.5(Kakkis, et al., Nucleic Acids Res. 16:7796 (1988)). The cassetteincluded 136 bp of the 3′ end of exon 2 and 242 bp of the 5′ end of exon3, which would remain in the properly spliced cDNA. No ATG sequences arepresent in the coding region of the intron cassette. The intron cassettewas cloned into the HinduIII site 5′ of the α-L-iduronidase cDNA. Theneo gene was deleted by digestion with Xhol followed by recircularizingthe vector to make pCMVhldu.

One vial of the working cell bank is thawed and placed in three T225flasks in DME/F12 or PF-CHO plus supplements, plus 5% FBS and 500 μg/mlG418. After 2-5 days, the cells are passaged using trypsin-EDTA to a1-liter spinner flask in the same medium for 2-5 days. The cells arethen transferred to two 3-liter spinner flasks for 2-5 days, followed byfour 8-liter spinner flasks for 2-5 days. The inoculum from the 8-literspinner flasks is added to two 110-liter Applikon® stirred tankbioreactors with an 80-90 liter working volume. Macroporous cellulosemicrocarriers are added at 2 grams per liter (160 grams), with PF-CHO orDME/F12 plus supplements, 5% FBS and 500 μg/ml of G418 at a final volumeof 80-90 liters. The flask is stirred by an overhead drive with a marineimpeller. The culture is monitored for agitation speed, temperature, DOand pH probes and controlled the Applikon® control system with a PCinterface. The parameters are controlled at the set points or range,35-37° C. depending on culture conditions, 40% air saturation, and pH6.95, using a heating blanket, oxygen sparger and base pump. The cultureis incubated for 3-5 days at which time the culture is emerging from thelog phase growth at 1-3×10⁶ cells per ml. Thereafter, perfusion isinitiated at an increasing rate with PF-CHO medium (with custommodifications, JRH Biosciences). The first four days of collection(range of 3-5 days) are set aside as “washout.” The collectionthereafter is the beginning of the production run. Production continueswith medium changes of as much as 2-3.5 culture volumes per day for20-36 days. The culture may be extended for 40 days or longer. Theculture is monitored for temperature, pH and DO on a continuous basis.The purification of the enzyme proceeds as described above. Collectedproduction medium containing iduronidase is then acidified to pH 5.3,filtered through a 0.2-micron filter and purified using Blue-Sepharosechromatography. The purified enzyme from multiple rounds ofBlue-Sepharose chromatography are then pooled and applied to a copperchelating column and eluted with glycerol in the buffer at a pH of 3.7.The enzyme is held at the acidic pH to inactivate potential viruses. Thecopper column eluate is then adjusted to pH 5.7 and 2 M NaCl and loadedon the phenyl Sepharose column. The enzyme is eluted at 0.7 M NaCl. Theeluate is concentrated and diafiltered into a formulation buffer of 150mM NaCl, 100 mM NaPO4, pH5.8. The enzyme is filtered through a 40 nMfilter to remove potential viruses and the filtrate adjusted to 0.001%polysorbate 80. The formulated enzyme is sterilely bulk filled intosterile polyethylene containers. The bulk enzyme is then filtered andfilled into 5 cc Type 1 glass vials appropriate for injectablepharmaceuticals, stoppered and capped.

EXAMPLE 2

For bioreactors using single cell suspensions, the seed train isprepared as described above in EXAMPLE 1. Using a single cell suspensionsimplifies bioreactor preparation and inoculation. The bioreactor isinoculated with cells in DMEM/F12 medium (25% of reactor volume) and JRH325 modified (25% of reactor volume). Medium equal to 50% of the workingreactor volume is added over 48 hours. Perfusion (and harvest) isstarted when cell density reaches 1.0 e⁶ and the perfusion medium is thesame as described above.

EXAMPLE 3

Short-term intravenous administration of purified human recombinantα-L-iduronidase to 9 MPS I dogs and 6 MPS I cats has shown significantuptake of an enzyme in a variety of tissues with an estimated 50% ormore recovery in tissues 24 hours after a single dose. Although liverand spleen take up the largest amount of enzymes, and have the bestpathologic improvement, improvements in pathology and glycosaminoglycancontent has been observed in many, but not all tissues. In particular,the cartilage, brain and heart valve did not have significantimprovement. Clinical improvement was observed in a single dog onlong-term treatment for 13 months, but other studies have been limitedto 6 months or less. All dogs, and most cats, that received recombinanthuman enzyme developed antibodies to the human product. The IgGantibodies are of the complement activating type (probable canine IgGequivalent). This phenomena is also observed in at least 13% ofalglucerase-treated Gaucher patients. Proteinuria has been observed inone dog which may be related to immune complex disease. No other effectsof the antibodies have been observed in the other treated animals.Specific toxicity was not observed and clinical laboratory studies(complete blood counts, electrolytes, BLJN/creatinine, liver enzymes,urinalysis) have been otherwise normal.

Enzyme therapy at even small doses of 25,000 units (0.1 mg/kg/wk)resulted in significant enzyme distribution to some tissues anddecreases in GAG storage. If continued for over 1 year, significantclinical effects of the therapy were evident in terms of activity, sizeand overall appearance of health. The therapy at this dose did notimprove other tissues that are important sites for disease in thisentity such as cartilage and brain. Higher doses of 125,000 units (0.5mg/kg) given 5 times over two weeks demonstrate that improved tissuepenetration can be achieved and a therapeutic effect at the tissue levelwas accomplished in as little as 2 weeks. Studies at this increased doseare ongoing in two dogs for six months to date. These MPS I dogs areshowing significant clinical improvement and substantial decreases inurinary GAG excretion into the normal range. Other than an immunereaction controlled by altered administration techniques, the enzymetherapy has not shown significant clinical or biochemical toxicity.Enzyme therapy at this higher weekly dose is effective at improving someclinical features of MPS I and decreasing storage without significanttoxicity.

The results of these various studies in MPS I dogs and one study in MPSI cats show that human recombinant α-L-iduronidase is safe. Althoughthese same results provide significant rationale that this recombinantenzyme should be effective in treating α-L-iduronidase deficiency, theydo not predict the clinical benefits or the potential immunologicalrisks of enzyme therapy in humans.

EXAMPLE 4

The human cDNA of α-L-iduronidase predicts a protein of 653 amino acidsand an expected molecular weight of 70,000 daltons after signal peptidecleavage. Amino acid sequencing reveals alanine 26 at the N-terminusgiving an expected protein of 629 amino acids. Human recombinantα-L-iduronidase has a Histidine at position 8 of the mature protein. Thepredicted protein sequence comprises six potential N-linkedoligosaccharide modification sites. All of these sites are modified inthe recombinant protein. The third and sixth sites have beendemonstrated to contain one or more mannose 6-phosphate residuesresponsible for high affinity uptake into cells.

This peptide corresponds to Amino Acids 26-45 of Human Recombinantα-L-iduronidase with an N-terminus alanine and the following sequence:

ala-glu-ala-pro-his-leu-val-his-val-asp-ala-ala-arg-ala-leu-trp-pro-leu-arg-arg(part of SEQ ID NO:2)

The recombinant enzyme has an apparent molecular weight of 82,000daltons on SDS-PAGE due to carbohydrate modifications. Purified humanrecombinant α-L-iduronidase has been sequenced by the UCLA ProteinSequencing facility. It is preferred to administer the recombinantenzyme intravenously. Human recombinant α-L-iduronidase was supplied forthe clinical trial in 10 mL polypropylene vials at a concentration of100,000-200,000 units per mL. The final dosage form of the enzyme usedin the clinical trial includes human recombinant α-L-iduronidase, normalsaline, and 100 mM phosphate buffer at pH 5.8. These are prepared in abag of normal saline. Polysorbate 80 at a final concentration of 0.001%was added to the formulation to stabilize the protein against shear,thereby avoiding precipitation in the final product vials.

Final Vial Formulation Currently in Use

Component Composition α-L-iduronidase Target to 0.7 mg/mL or 100 (new)units per mL Sodium chloride solution 150 mM Sodium phosphate buffer 100mM, pH 5.8 Polysorbate 80 0.001%

Final Dosage Form Used in the Treatment of Patients

Component Composition α-L-iduronidase product 5-12 fold dilution of vialconcentration Sodium chloride solution 50 mM Sodium phosphate buffer bag100-250 cc IV Human albumin 1 mg/ml

EXAMPLE 5 Effects of Intravenous Administration of α-L-Iduronidase inPatients with Mucopolysaccharidosis I

Based on studies of cloning of cDNA encoding α-L-iduronidase (Scott, etal., Proc. Natl. Acad. Sci. USA 88: 9695-99 (1991); Stoltzftls, et al.,J. Biol. Chem. 267: 6570-75 (1992)) and animal studies showing effectsof α-L-iduronidase to reduce lysosomal storage in many tissues (Shull,et al., Proc. Natl. Acad. Sci. USA 91: 12937-41 (1994); Kakkis, et al.,Biochem. Mol. Med. 58: 156-67 (1996)), a 52-week study was conducted toassess the safety and clinical efficacy of intravenous administration ofhighly purified α-L-iduronidase in ten patients withmucopolysaccharidosis I (MPS I).

Recombinant human α-L-iduronidase was produced and purified to greaterthan 97-99%. Patients demonstrated typical clinical manifestations ofthe disorder and diagnosis was confirmed by biochemical determination ofα-L-iduronidase deficiency in leukocytes.

Patients were given recombinant human α-L-iduronidase (diluted in normalsaline with 0.1% human serum albumin) intravenously at a dose of 125,000units per kg (using original assay and unit definition); 3,000 units perkg were given over the first hour, and 61,000 units per kg in each ofthe following two hours. The dose of 125,000 units per kg is equivalentto 100 SI units per kg using the new assay. The infusions were prolongedup to 4-6 hours in patients who had hypersensitivity reactions.

At baseline and at 6, 12, 26 and 52 weeks depending on the evaluation,the patients underwent examinations including history, physicalexaminations by specialists, echocardiography, EKG, MRI, polysomnography(weeks 0 and 26), skeletal survey (weeks 0, 26, 52), range of motionmeasurements, corneal photographs, and skin biopsy (week 0) to set upfibroblast cultures for enzyme determination and genotyping. Range ofmotion measurements were performed with a goniometer and the maximumactive (patient initiated) range was recorded for each motion. Shoulderflexion is movement of the elbow anteriorly from the side of the bodyand elbow and knee extension represent straightening of the joint.Degrees of restriction represent the difference between the normalmaximum range of motion for age and the measured value. Polysomnographywas performed according to American Thoracic Society guidelines andapneic events (cessation of oro-nasal airflow for 10 seconds or more),hypopneic events (decreased oro-nasal airflow of 50% or more withdesaturation of 2% or more, or evidence of arousal), minutes below 89%oxygen saturation and total sleep time recorded among the standardmeasurements required. From these data an apnea/hypopnea index wascalculated by dividing the total number of apneic and hypopneic eventsby the number of hours of sleep. Biochemical studies includedmeasurement of enzyme activity in leukocytes and brushings of buccalmucosal, urinary glycosaminoglycan levels, and tests for serumantibodies to recombinant human α-L-iduronidase (ELISA and Westernblot). Organ volumes were determined by analysis of MRI digital imagedata using Advantage Windows workstation software from General Electric.The organ volume was measured in milliliters and was converted to weightassuming a density of 1 gram per ml. Urinary glycosaminoglycan excretionwas assayed by an adaptation of a published method. Western blots andELISA assays for antibodies to recombinant human α-L-iduronidase wereperformed by standard methods. Uronic acids and N-sulfate of urinaryglycosaminoglycans were analyzed by the orcinol, carbazole and MBTHmethods, and by electrophoretic separations.

All patients received weekly infusions of recombinant humanα-L-iduronidase administered for 52 weeks. The mean activity ofα-L-iduronidase in leukocytes was 0.04 units per mg before treatment andwhen measured on average 7 days after an infusion (i.e. immediatelybefore the next infusion), 4.98 units per mg, or 15.0 percent of normal.Enzyme activity was not detectable in buccal brushings prior totreatment, but 7 days after infusions it reached a level of 1 percent ofnormal.

Liver volume decreased by 19 to 37 percent from baseline in 9 patientsand 5 percent in one patient at 52 weeks; the mean decrease was 25.0percent (n=10, P<0.001). By 26 weeks, liver size was normal for bodyweight and age in 8 patients (FIG. 1). In 2 patients (patients 6 and 9)with the largest relative liver size at baseline, liver size was closeto normal at 52 weeks (3.2 and 3.3 percent of body weight,respectively). Spleen size decreased in 8 patients by 13 to 42 percentfrom baseline (mean decrease of 20 percent in 10 patients, P<0.001).

Urinary glycosaminoglycan excretion declined rapidly by 3 to 4 weeks andby 8-12 weeks had fallen by 60-80 percent of baseline. At 52 weeks, themean reduction was 63 percent (range 53-74; p<0.001). Eight of tenpatients had a 75 percent or greater reduction of the baseline amount ofurinary glycosaminoglycan in excess of the upper limit of normal forage. The results were confirmed by assay of uronic acids and N-sulfate(a test specific for heparan sulfate). Electrophoresis studies of urinedetected a significant reduction in heparan sulfate and dermatan sulfateexcretion but some excess dermatan sulfate excretion persisted in allpatients.

The mean height increased 6.0 cm (5.2 percent) in the 6 prepubertalpatients (Table 2) and their mean height growth velocity increased from2.8 cm/yr to 5.2 cm/yr during treatment (P=0.011). For all 10 patients,mean body weight increased 3.2 kg (8.8 percent) and the mean increasewas 4.2 kg (17.1 percent) for the 6 prepubertal patients (Table 2). Inthese 6 patients, the mean pretreatment weight growth velocity increasedfrom 1.7 kg per year to 3.8 kg per year during treatment (P=0.04).

Shoulder flexion (moving the elbow anteriorly) increased in 6 of the 8subjects evaluated at baseline with a mean improvement for the right andleft shoulders of 28° and 26°, respectively (P<0.002; FIG. 2). Elbowextension and knee extension increased by a mean of 7.0° (P<0.03) and3.2° (P=0.10), respectively, in the 10 patients (FIG. 2).

Analysis of the improvement in individual patients revealed that themost restricted joints had the greatest improvement. For example atbaseline, patients 5, 9 and 10 could not flex their shoulders (move theelbow anteriorly) beyond 100°, which increased 21° to 51° aftertreatment. Similarly, patients 2 and 9 had a substantial increase inknee extension. The changes in range of motion were accompanied bypatient-reported increases in physical activities such as being able towash their hair, hold a hamburger normally, hang from monkey bars, andplay sports better.

Seven patients had a decrease in apnea and hypopnea events from 155 to60 per night upon treatment (a 61 percent decrease) with a change inmean apnea/hypopnea index (total number of events per hour) from 2.1 to1.0. Three patients had clinically significant sleep apnea and all threeimproved during treatment. In patient 2, the apnea/hypopnea indexdecreased from 4.5 at baseline to 0.4 at 26 weeks and total time ofoxygen desaturation decreased from 48 minutes to 1 minute per night.Patient 6 required nightly continuous positive airway pressure therapybefore treatment due to severe desaturation (61 minutes below 89 percentsaturation with continuous positive airway pressure in 368 minutes ofsleep), but by 52 weeks, the patient tolerated the sleep study withoutCPAP and desaturated below 89 percent for only 8 minutes during 332minutes of sleep. Patient 9 had an apnea hypopnea index of 9.5 whichdecreased to 4.0 by 26 weeks. Patient 8 worsened with an apnea hypopneaindex of 0.1 increasing to 3.1 at 26 weeks and 9.3 at 52 weeks forunclear reasons. Eight of ten patients or their families reportedimproved breathing, and 5 of 7 noted quieter nighttime breathing,improved sleep quality and decreased daytime somnolence.

New York Heart Association functional classification was determined byserial patient interviews. All 10 patients reported improvement by oneor two classes but there was no significant objective data fromechocardiographic studies to verify direct cardiac benefit. The improvedfunctional scores may reflect improvements in other aspects of MPS Idisease rather than cardiac function. Comparing baseline to 52 weeks oftreatment, echocardiography demonstrated decreased tricuspidregurgitation or pulmonic regurgitation in 4 patients but two patients(patients 2 and 7) had worsening mitral regurgitation. At baseline,patient 6 had atrial flutter and clinical signs of cardiac failureincluding dyspnea at rest and peripheral edema. By 12 weeks, he hadnormal sinus rhythm with first degree block and his dyspnea at rest andpitting edema resolved.

All 10 patients reported a lack of endurance and limitations of dailyactivities before treatment but exercise tolerance was not formallytested. During treatment, all patients improved and by 26 weeks, manywere able to walk more, run and play sports. Patients 3, 4 and 5reported the resolution of severe incapacitating headaches aftertreatment for 6-12 weeks.

Several patients reported decreased photophobia or conjunctivalirritation. Visual acuity improved in one patient (20/1000 to 20/200 inone eye) and modestly in 2 others.

The results of this study indicate that intravenous administration ofthe highly purified recombinant human α-L-iduronidase of the presentinvention results in clinical and biochemical improvement in patientswith Mucopolysaccharidosis I. The normalization of liver size and nearnormalization of urinary glycosaminoglycan excretion is consistent withdata from studies in dogs with Mucopolysaccharidosis I, whichdemonstrated clearance of storage in the liver and decreased urinaryglycosaminoglycan excretion in as little as 2 weeks.

Hypersensitivity reactions to the infusions of recombinant humanα-L-iduronidase were less severe than predicted from studies in dogs.Though important in some patients, recurrent urticaria was manageablewith premedication and adjustments in infusion rate. Antibodies specificto α-L-iduronidase were detected in 4 patients with usually subclinicalcomplement activation, and both the antibodies and complement activationdeclined with time. Similar IgG-mediated immune responses have beenpreviously noted in patients with Gaucher disease treat withglucocerebrosidase, although the events were more frequent in ourpatients. Mucopolysaccharidosis I patients with a null genotype may havea greater immune response than in these 10 patients, none of whom has anull.

Thus, recombinant human α-L-iduronidase can reduce lysosomal storage andameliorates some aspects of clinical disease of Mucopolysaccharidosis I.

The invention, and the manner and process of making and using it, arenow described in such full, clear, concise and exact terms as to enableany person skilled in the art to which it pertains, to make and use thesame. It is to be understood that the foregoing describes preferredembodiments of the present invention and that modifications may be madetherein without departing from the spirit or scope of the presentinvention as set forth in the claims. To particularly point out anddistinctly claim the subject matter regarded as invention, the followingclaims conclude this specification.

2 1 6200 DNA Homo sapiens CDS (1558)...(3516) 1 gacggatcgg gagatctcccgatcccctat ggtcgactct cagtacaatc tgctctgatg 60 ccgcatagtt aagccagtatctgctccctg cttgtgtgtt ggaggtcgct gagtagtgcg 120 cgagcaaaat ttaagctacaacaaggcaag gcttgaccga caattgcatg aagaatctgc 180 ttagggttag gcgttttgcgctgcttcgcg atgtacgggc cagatatacg cgttgacatt 240 gattattgac tagttattaatagtaatcaa ttacggggtc attagttcat agcccatata 300 tggagttccg cgttacataacttacggtaa atggcccgcc tggctgaccg cccaacgacc 360 cccgcccatt gacgtcaataatgacgtatg ttcccatagt aacgccaata gggactttcc 420 attgacgtca atgggtggactatttacggt aaactgccca cttggcagta catcaagtgt 480 atcatatgcc aagtacgccccctattgacg tcaatgacgg taaatggccc gcctggcatt 540 atgcccagta catgaccttatgggactttc ctacttggca gtacatctac gtattagtca 600 tcgctattac catggtgatgcggttttggc agtacatcaa tgggcgtgga tagcggtttg 660 actcacgggg atttccaagtctccacccca ttgacgtcaa tgggagtttg ttttggcacc 720 aaaatcaacg ggactttccaaaatgtcgta acaactccgc cccattgacg caaatgggcg 780 gtaggcgtgt acggtgggaggtctatataa gcagagctct ctggctaact agagaaccca 840 ctgcttaact ggcttatcgaaattaatacg actcactata gggagaccca agcttcgcag 900 aattcctgcg gctgctacagtgtgtccagc gtcctgcctg gctgtgctga gcgctggaac 960 agtggcgcat cattcaagtgcacagttacc catcctgagt ctggcacctt aactggcaca 1020 attgccaaag tcacaggtgagctcagatgc ataccaggac attgtatgac gttccctgct 1080 cacatgcctg ctttcttcctataatacaga tggtcaacta actgctcatg tccttatatc 1140 acagagggaa attggagctatctgaggaac tgcccagaag ggaagggcag aggggtcttg 1200 ctctccttgt ctgagccataactcttcttt ctaccttcca gtgaacacct tcccacccca 1260 ggtccacctg ctaccgccgccgtcggagga gctggccctg aatgagctct tgtccctgac 1320 atgcctggtg cgagctttcaaccctaaaga agtgctggtg cgatggctgc atggaaatga 1380 ggagctgtcc ccagaaagctacctagtgtt tgagccccta aaggagccag gcgagggagc 1440 caccacctac ctggtgacaagcgtgttgcg tgtatcagct gaaagcttga tatcgaattc 1500 cggaggcgga accggcagtgcagcccgaag ccccgcagtc cccgagcacg cgtggcc atg 1560 Met 1 cgt ccc ctg cgcccc cgc gcc gcg ctg ctg gcg ctc ctg gcc tcg ctc 1608 Arg Pro Leu Arg ProArg Ala Ala Leu Leu Ala Leu Leu Ala Ser Leu 5 10 15 ctg gcc gcg ccc ccggtg gcc ccg gcc gag gcc ccg cac ctg gtg cat 1656 Leu Ala Ala Pro Pro ValAla Pro Ala Glu Ala Pro His Leu Val His 20 25 30 gtg gac gcg gcc cgc gcgctg tgg ccc ctg cgg cgc ttc tgg agg agc 1704 Val Asp Ala Ala Arg Ala LeuTrp Pro Leu Arg Arg Phe Trp Arg Ser 35 40 45 aca ggc ttc tgc ccc ccg ctgcca cac agc cag gct gac cag tac gtc 1752 Thr Gly Phe Cys Pro Pro Leu ProHis Ser Gln Ala Asp Gln Tyr Val 50 55 60 65 ctc agc tgg gac cag cag ctcaac ctc gcc tat gtg ggc gcc gtc cct 1800 Leu Ser Trp Asp Gln Gln Leu AsnLeu Ala Tyr Val Gly Ala Val Pro 70 75 80 cac cgc ggc atc aag cag gtc cggacc cac tgg ctg ctg gag ctt gtc 1848 His Arg Gly Ile Lys Gln Val Arg ThrHis Trp Leu Leu Glu Leu Val 85 90 95 acc acc agg ggg tcc act gga cgg ggcctg agc tac aac ttc acc cac 1896 Thr Thr Arg Gly Ser Thr Gly Arg Gly LeuSer Tyr Asn Phe Thr His 100 105 110 ctg gac ggg tac ctg gac ctt ctc agggag aac cag ctc ctc cca ggg 1944 Leu Asp Gly Tyr Leu Asp Leu Leu Arg GluAsn Gln Leu Leu Pro Gly 115 120 125 ttt gag ctg atg ggc agc gcc tcg ggccac ttc act gac ttt gag gac 1992 Phe Glu Leu Met Gly Ser Ala Ser Gly HisPhe Thr Asp Phe Glu Asp 130 135 140 145 aag cag cag gtg ttt gag tgg aaggac ttg gtc tcc agc ctg gcc agg 2040 Lys Gln Gln Val Phe Glu Trp Lys AspLeu Val Ser Ser Leu Ala Arg 150 155 160 aga tac atc ggt agg tac gga ctggcg cat gtt tcc aag tgg aac ttc 2088 Arg Tyr Ile Gly Arg Tyr Gly Leu AlaHis Val Ser Lys Trp Asn Phe 165 170 175 gag acg tgg aat gag cca gac caccac gac ttt gac aac gtc tcc atg 2136 Glu Thr Trp Asn Glu Pro Asp His HisAsp Phe Asp Asn Val Ser Met 180 185 190 acc atg caa ggc ttc ctg aac tactac gat gcc tgc tcg gag ggt ctg 2184 Thr Met Gln Gly Phe Leu Asn Tyr TyrAsp Ala Cys Ser Glu Gly Leu 195 200 205 cgc gcc gcc agc ccc gcc ctg cggctg gga ggc ccc ggc gac tcc ttc 2232 Arg Ala Ala Ser Pro Ala Leu Arg LeuGly Gly Pro Gly Asp Ser Phe 210 215 220 225 cac agg cca ccg cga tcc ccgctg agc tgg ggc ctc ctg cgc cac tgc 2280 His Arg Pro Pro Arg Ser Pro LeuSer Trp Gly Leu Leu Arg His Cys 230 235 240 cac gac ggt acc aac ttc ttcact ggg gag gcg ggc gtg cgg ctg gac 2328 His Asp Gly Thr Asn Phe Phe ThrGly Glu Ala Gly Val Arg Leu Asp 245 250 255 tac atc tcc ctc cac agg aagggt gcg cgc agc tcc atc tcc atc ctg 2376 Tyr Ile Ser Leu His Arg Lys GlyAla Arg Ser Ser Ile Ser Ile Leu 260 265 270 gag cag gag aag gtc gtc gcgcag cag atc cgg cag ctc ttc ccc aag 2424 Glu Gln Glu Lys Val Val Ala GlnGln Ile Arg Gln Leu Phe Pro Lys 275 280 285 ttc gcg gac acc ccc att tacaac gac gag gcg gac ccg ctg gtg ggc 2472 Phe Ala Asp Thr Pro Ile Tyr AsnAsp Glu Ala Asp Pro Leu Val Gly 290 295 300 305 tgg tcc ctg cca cag ccgtgg agg gcg gac gtg acc tac gcg gcc atg 2520 Trp Ser Leu Pro Gln Pro TrpArg Ala Asp Val Thr Tyr Ala Ala Met 310 315 320 gtg gtg aag gtc atc gcgcag cat cag aac ctg cta ctg gcc aac acc 2568 Val Val Lys Val Ile Ala GlnHis Gln Asn Leu Leu Leu Ala Asn Thr 325 330 335 acc tcc gcc ttc ccc tacgcg ctc ctg agc aac gac aat gcc ttc ctg 2616 Thr Ser Ala Phe Pro Tyr AlaLeu Leu Ser Asn Asp Asn Ala Phe Leu 340 345 350 agc tac cac ccg cac cccttc gcg cag cgc acg ctc acc gcg cgc ttc 2664 Ser Tyr His Pro His Pro PheAla Gln Arg Thr Leu Thr Ala Arg Phe 355 360 365 cag gtc aac aac acc cgcccg ccg cac gtg cag ctg ttg cgc aag ccg 2712 Gln Val Asn Asn Thr Arg ProPro His Val Gln Leu Leu Arg Lys Pro 370 375 380 385 gtg ctc acg gcc atgggg ctg ctg gcg ctg ctg gat gag gag cag ctc 2760 Val Leu Thr Ala Met GlyLeu Leu Ala Leu Leu Asp Glu Glu Gln Leu 390 395 400 tgg gcc gaa gtg tcgcag gcc ggg acc gtc ctg gac agc aac cac acg 2808 Trp Ala Glu Val Ser GlnAla Gly Thr Val Leu Asp Ser Asn His Thr 405 410 415 gtg ggc gtc ctg gccagc gcc cac cgc ccc cag ggc ccg gcc gac gcc 2856 Val Gly Val Leu Ala SerAla His Arg Pro Gln Gly Pro Ala Asp Ala 420 425 430 tgg cgc gcc gcg gtgctg atc tac gcg agc gac gac acc cgc gcc cac 2904 Trp Arg Ala Ala Val LeuIle Tyr Ala Ser Asp Asp Thr Arg Ala His 435 440 445 ccc aac cgc agc gtcgcg gtg acc ctg cgg ctg cgc ggg gtg ccc ccc 2952 Pro Asn Arg Ser Val AlaVal Thr Leu Arg Leu Arg Gly Val Pro Pro 450 455 460 465 ggc ccg ggc ctggtc tac gtc acg cgc tac ctg gac aac ggg ctc tgc 3000 Gly Pro Gly Leu ValTyr Val Thr Arg Tyr Leu Asp Asn Gly Leu Cys 470 475 480 agc ccc gac ggcgag tgg cgg cgc ctg ggc cgg ccc gtc ttc ccc acg 3048 Ser Pro Asp Gly GluTrp Arg Arg Leu Gly Arg Pro Val Phe Pro Thr 485 490 495 gca gag cag ttccgg cgc atg cgc gcg gct gag gac ccg gtg gcc gcg 3096 Ala Glu Gln Phe ArgArg Met Arg Ala Ala Glu Asp Pro Val Ala Ala 500 505 510 gcg ccc cgc ccctta ccc gcc ggc ggc cgc ctg acg ctg cgc ccc gcg 3144 Ala Pro Arg Pro LeuPro Ala Gly Gly Arg Leu Thr Leu Arg Pro Ala 515 520 525 ctg cgg ctg ccgtcg ctt ttg ctg gtg cac gtg tgt gcg cgc ccc gag 3192 Leu Arg Leu Pro SerLeu Leu Leu Val His Val Cys Ala Arg Pro Glu 530 535 540 545 aag ccg cccggg cag gtc acg cgg ctc cgc gcc ctg ccc ctg acc caa 3240 Lys Pro Pro GlyGln Val Thr Arg Leu Arg Ala Leu Pro Leu Thr Gln 550 555 560 ggg cag ctggtt ctg gtc tgg tcg gat gaa cac gtg ggc tcc aag tgc 3288 Gly Gln Leu ValLeu Val Trp Ser Asp Glu His Val Gly Ser Lys Cys 565 570 575 ctg tgg acatac gag atc cag ttc tct cag gac ggt aag gcg tac acc 3336 Leu Trp Thr TyrGlu Ile Gln Phe Ser Gln Asp Gly Lys Ala Tyr Thr 580 585 590 ccg gtc agcagg aag cca tcg acc ttc aac ctc ttt gtg ttc agc cca 3384 Pro Val Ser ArgLys Pro Ser Thr Phe Asn Leu Phe Val Phe Ser Pro 595 600 605 gac aca ggtgct gtc tct ggc tcc tac cga gtt cga gcc ctg gac tac 3432 Asp Thr Gly AlaVal Ser Gly Ser Tyr Arg Val Arg Ala Leu Asp Tyr 610 615 620 625 tgg gcccga cca ggc ccc ttc tcg gac cct gtg ccg tac ctg gag gtc 3480 Trp Ala ArgPro Gly Pro Phe Ser Asp Pro Val Pro Tyr Leu Glu Val 630 635 640 cct gtgcca aga ggg ccc cca tcc ccg ggc aat cca tgagcctgtg 3526 Pro Val Pro ArgGly Pro Pro Ser Pro Gly Asn Pro 645 650 ctgagcccca gtgggttgca cctccaccggcagtcagcga gctggggctg cactgtgccc 3586 atgctgccct cccatcaccc cctttgcaatatatttttat attttaaaaa aaaaaaaaaa 3646 aaaaaaaaaa aaaaaaaaaa aaaaaaaaaaaaaaaaaaaa aaaaaaaaaa aaagaattcc 3706 tgcagcccgg gggatccact agttctagagggcccgttta aacccgctga tcagcctcga 3766 ctgtgccttc tagttgccag ccatctgttgtttgcccctc ccccgtgcct tccttgaccc 3826 tggaaggtgc cactcccact gtcctttcctaataaaatga ggaaattgca tcgcattgtc 3886 tgagtaggtg tcattctatt ctggggggtggggtggggca ggacagcaag ggggaggatt 3946 gggaagacaa tagcaggcat gctggggatgcggtgggctc tatggcttct gaggcggaaa 4006 gaaccagctg gggctcgaga gcttggcgtaatcatggtca tagctgtttc ctgtgtgaaa 4066 ttgttatccg ctcacaattc cacacaacatacgagccgga agcataaagt gtaaagcctg 4126 gggtgcctaa tgagtgagct aactcacattaattgcgttg cgctcactgc ccgctttcca 4186 gtcgggaaac ctgtcgtgcc agctgcattaatgaatcggc caacgcgcgg ggagaggcgg 4246 tttgcgtatt gggcgctctt ccgcttcctcgctcactgac tcgctgcgct cggtcgttcg 4306 gctgcggcga gcggtatcag ctcactcaaaggcggtaata cggttatcca cagaatcagg 4366 ggataacgca ggaaagaaca tgtgagcaaaaggccagcaa aaggccagga accgtaaaaa 4426 ggccgcgttg ctggcgtttt tccataggctccgcccccct gacgagcatc acaaaaatcg 4486 acgctcaagt cagaggtggc gaaacccgacaggactataa agataccagg cgtttccccc 4546 tggaagctcc ctggtgcgct ctcctgttccgaccctgccg cttaccggat acctgtccgc 4606 ctttctccct tcgggaagcg tggcgctttctcaatgctca cgctgtaggt atctcagttc 4666 ggtgtaggtc gttcgctcca agctgggctgtgtgcacgaa ccccccgttc agcccgaccg 4726 ctgcgcctta tccggtaact atcgtcttgagtccaacccg gtaagacacg acttatcgcc 4786 actggcagca gccactggta acaggattagcagagcgagg tatgtaggcg gtgctacaga 4846 gttcttgaag tggtggccta actacggctacactagaagg acagtatttg gtatctgcgc 4906 tctgctgaag ccagttacct tcggaaaaagagttggtagc tcttgatccg gcaaacaaac 4966 caccgctggt agcggtggtt tttttgtttgcaagcagcag attacgcgca gaaaaaaagg 5026 atctcaagaa gatcctttga tcttttctacggggtctgac gctcagtgga acgaaaactc 5086 acgttaaggg attttggtca tgagattatcaaaaaggatc ttcacctaga tccttttaaa 5146 ttaaaaatga agttttaaat caatctaaagtatatatgag taaacttggt ctgacagtta 5206 ccaatgctta atcagtgagg cacctatctcagcgatctgt ctatttcgtt catccatagt 5266 tgcctgactc cccgtcgtgt agataactacgatacgggag ggcttaccat ctggccccag 5326 tgctgcaatg ataccgcgag acccacgctcaccggctcca gatttatcag caataaacca 5386 gccagccgga agggccgagc gcagaagtggtcctgcaact ttatccgcct ccatccagtc 5446 tattaattgt tgccgggaag ctagagtaagtagttcgcca gttaatagtt tgcgcaacgt 5506 tgttgccatt gctacaggca tcgtggtgtcacgctcgtcg tttggtatgg cttcattcag 5566 ctccggttcc caacgatcaa ggcgagttacatgatccccc atgttgtgca aaaaagcggt 5626 tagctccttc ggtcctccga tcgttgtcagaagtaagttg gccgcagtgt tatcactcat 5686 ggttatggca gcactgcata attctgttactgtcatgcca tccgtaagat gcttttctgt 5746 gactggtgag tactcaacca agtcattctgagaatagtgt atgcggcgac cgagttgctc 5806 ttgcccggcg tcaatacggg ataataccgcgccacatagc agaactttaa aagtgctcat 5866 cattggaaaa cgttcttcgg ggcgaaaactctcaaggatc ttaccgctgt tgagatccag 5926 ttcgatgtaa cccactcgtg cacccaactgatcttcagca tcttttactt tcaccagcgt 5986 ttctgggtga gcaaaaacag gaaggcaaaatgccgcaaaa aagggaataa gggcgacacg 6046 gaaatgttga atactcatac tcttcctttttcaatattat tgaagcattt atcagggtta 6106 ttgtctcatg agcggataca tatttgaatgtatttagaaa aataaacaaa taggggttcc 6166 gcgcacattt ccccgaaaag tgccacctgacgtc 6200 2 653 PRT Homo sapiens 2 Met Arg Pro Leu Arg Pro Arg Ala AlaLeu Leu Ala Leu Leu Ala Ser 1 5 10 15 Leu Leu Ala Ala Pro Pro Val AlaPro Ala Glu Ala Pro His Leu Val 20 25 30 His Val Asp Ala Ala Arg Ala LeuTrp Pro Leu Arg Arg Phe Trp Arg 35 40 45 Ser Thr Gly Phe Cys Pro Pro LeuPro His Ser Gln Ala Asp Gln Tyr 50 55 60 Val Leu Ser Trp Asp Gln Gln LeuAsn Leu Ala Tyr Val Gly Ala Val 65 70 75 80 Pro His Arg Gly Ile Lys GlnVal Arg Thr His Trp Leu Leu Glu Leu 85 90 95 Val Thr Thr Arg Gly Ser ThrGly Arg Gly Leu Ser Tyr Asn Phe Thr 100 105 110 His Leu Asp Gly Tyr LeuAsp Leu Leu Arg Glu Asn Gln Leu Leu Pro 115 120 125 Gly Phe Glu Leu MetGly Ser Ala Ser Gly His Phe Thr Asp Phe Glu 130 135 140 Asp Lys Gln GlnVal Phe Glu Trp Lys Asp Leu Val Ser Ser Leu Ala 145 150 155 160 Arg ArgTyr Ile Gly Arg Tyr Gly Leu Ala His Val Ser Lys Trp Asn 165 170 175 PheGlu Thr Trp Asn Glu Pro Asp His His Asp Phe Asp Asn Val Ser 180 185 190Met Thr Met Gln Gly Phe Leu Asn Tyr Tyr Asp Ala Cys Ser Glu Gly 195 200205 Leu Arg Ala Ala Ser Pro Ala Leu Arg Leu Gly Gly Pro Gly Asp Ser 210215 220 Phe His Arg Pro Pro Arg Ser Pro Leu Ser Trp Gly Leu Leu Arg His225 230 235 240 Cys His Asp Gly Thr Asn Phe Phe Thr Gly Glu Ala Gly ValArg Leu 245 250 255 Asp Tyr Ile Ser Leu His Arg Lys Gly Ala Arg Ser SerIle Ser Ile 260 265 270 Leu Glu Gln Glu Lys Val Val Ala Gln Gln Ile ArgGln Leu Phe Pro 275 280 285 Lys Phe Ala Asp Thr Pro Ile Tyr Asn Asp GluAla Asp Pro Leu Val 290 295 300 Gly Trp Ser Leu Pro Gln Pro Trp Arg AlaAsp Val Thr Tyr Ala Ala 305 310 315 320 Met Val Val Lys Val Ile Ala GlnHis Gln Asn Leu Leu Leu Ala Asn 325 330 335 Thr Thr Ser Ala Phe Pro TyrAla Leu Leu Ser Asn Asp Asn Ala Phe 340 345 350 Leu Ser Tyr His Pro HisPro Phe Ala Gln Arg Thr Leu Thr Ala Arg 355 360 365 Phe Gln Val Asn AsnThr Arg Pro Pro His Val Gln Leu Leu Arg Lys 370 375 380 Pro Val Leu ThrAla Met Gly Leu Leu Ala Leu Leu Asp Glu Glu Gln 385 390 395 400 Leu TrpAla Glu Val Ser Gln Ala Gly Thr Val Leu Asp Ser Asn His 405 410 415 ThrVal Gly Val Leu Ala Ser Ala His Arg Pro Gln Gly Pro Ala Asp 420 425 430Ala Trp Arg Ala Ala Val Leu Ile Tyr Ala Ser Asp Asp Thr Arg Ala 435 440445 His Pro Asn Arg Ser Val Ala Val Thr Leu Arg Leu Arg Gly Val Pro 450455 460 Pro Gly Pro Gly Leu Val Tyr Val Thr Arg Tyr Leu Asp Asn Gly Leu465 470 475 480 Cys Ser Pro Asp Gly Glu Trp Arg Arg Leu Gly Arg Pro ValPhe Pro 485 490 495 Thr Ala Glu Gln Phe Arg Arg Met Arg Ala Ala Glu AspPro Val Ala 500 505 510 Ala Ala Pro Arg Pro Leu Pro Ala Gly Gly Arg LeuThr Leu Arg Pro 515 520 525 Ala Leu Arg Leu Pro Ser Leu Leu Leu Val HisVal Cys Ala Arg Pro 530 535 540 Glu Lys Pro Pro Gly Gln Val Thr Arg LeuArg Ala Leu Pro Leu Thr 545 550 555 560 Gln Gly Gln Leu Val Leu Val TrpSer Asp Glu His Val Gly Ser Lys 565 570 575 Cys Leu Trp Thr Tyr Glu IleGln Phe Ser Gln Asp Gly Lys Ala Tyr 580 585 590 Thr Pro Val Ser Arg LysPro Ser Thr Phe Asn Leu Phe Val Phe Ser 595 600 605 Pro Asp Thr Gly AlaVal Ser Gly Ser Tyr Arg Val Arg Ala Leu Asp 610 615 620 Tyr Trp Ala ArgPro Gly Pro Phe Ser Asp Pro Val Pro Tyr Leu Glu 625 630 635 640 Val ProVal Pro Arg Gly Pro Pro Ser Pro Gly Asn Pro 645 650

What is claimed is:
 1. A method of purifying human recombinantα-L-iduronidase having a purity of equal to or greater than about 99%purity, comprising the steps of: (a) harvesting and filtering fluidobtained from a culture of Chinese hamster ovary cells transformed withnucleic acids encoding said human recombinant α-L-iduronidase; (b)adjusting the pH of the fluid to an acidic pH wherein any potentialvirus is inactivated and said human recombinant α-L-iduronidase is notharmed, followed by filtration through a 0.2 micron to 0.54 micronfilter; (c) passing the fluid from step (b) through a Cibracon blue dyeinteraction chromatography column to capture said human recombinantα-L-iduronidase; (d) passing the fluid through a copper chelationchromatography column to remove contaminating Chinese hamster ovaryproteins; (e) passing the fluid through a phenyl hydrophobic interactionchromatography column to reduce residual leached Cibacron blue dye andcopper ions canned over from previous columns; and (f) concentrating anddiafiltering the purified human recombinant α-L-iduronidase; whereinsaid purity of equal to or greater than about 99% purity of humanrecombinant α-L-iduronidase is measured by μg of contaminating Chinesehamster ovary protein per mg of total protein.
 2. The method of claim 1,wherein said Cibracon blue dye interaction chromatography column is usedto purify said human α-L-iduronidase seven to ten fold.
 3. The method ofclaim 1, wherein said method comprises using 10% glycerol in all buffersto increase the quantitative recovery of said human α-L-iduronidase. 4.The method of claim 1, wherein step (b) results in the pH of the fluidadjusted to pH 5.3.
 5. The method of claim 1, wherein said purifiedhuman recombinant α-L-iduronidase has a specific activity greater than200,000 units per milligram protein.
 6. The method of claim 5, whereinsaid purified human recombinant α-L-iduronidase has a specific activitygreater than 240,000 units per milligram protein.
 7. The method of claim6, wherein said purified human recombinant α-L-iduronidase comprises oneor more mannose-6-phosphate residues.
 8. The method of claim 7, whereinsaid purified human recombinant α-L-iduronidase comprises amannose-6-phosphate residue attached at position 3 and amannose-6-phosphate residue attached at position
 6. 9. The method ofclaim 1, wherein said purified human recombinant α-L-iduronidase has ahalf-life inside a cell of approximately 5 days.
 10. The method of claim1, wherein said human recombinant α-L-iduronidase comprises the aminoacid sequence of residues 26 to 653 of SEQ ID NO:2.